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EP0524501B1 - Verfahren zur Herstellung von Allophanat- und Isocyanuratgruppen enthaltenden Polyisocyanaten - Google Patents

Verfahren zur Herstellung von Allophanat- und Isocyanuratgruppen enthaltenden Polyisocyanaten Download PDF

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Publication number
EP0524501B1
EP0524501B1 EP19920111701 EP92111701A EP0524501B1 EP 0524501 B1 EP0524501 B1 EP 0524501B1 EP 19920111701 EP19920111701 EP 19920111701 EP 92111701 A EP92111701 A EP 92111701A EP 0524501 B1 EP0524501 B1 EP 0524501B1
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Prior art keywords
trimerization
groups
catalyst
carbon atoms
reaction
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French (fr)
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EP0524501B2 (de
EP0524501A1 (de
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Terry A. Potter
William A. Slack
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Bayer Corp
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Bayer AG
Bayer Corp
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
    • C08G18/78—Nitrogen
    • C08G18/79—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates
    • C08G18/791—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups
    • C08G18/792—Nitrogen characterised by the polyisocyanates used, these having groups formed by oligomerisation of isocyanates or isothiocyanates containing isocyanurate groups formed by oligomerisation of aliphatic and/or cycloaliphatic isocyanates or isothiocyanates
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07D—HETEROCYCLIC COMPOUNDS
    • C07D251/00—Heterocyclic compounds containing 1,3,5-triazine rings
    • C07D251/02—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings
    • C07D251/12—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members
    • C07D251/26—Heterocyclic compounds containing 1,3,5-triazine rings not condensed with other rings having three double bonds between ring members or between ring members and non-ring members with only hetero atoms directly attached to ring carbon atoms
    • C07D251/30—Only oxygen atoms
    • C07D251/34—Cyanuric or isocyanuric esters
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/02—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only
    • C08G18/022—Polymeric products of isocyanates or isothiocyanates of isocyanates or isothiocyanates only the polymeric products containing isocyanurate groups
    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08G—MACROMOLECULAR COMPOUNDS OBTAINED OTHERWISE THAN BY REACTIONS ONLY INVOLVING UNSATURATED CARBON-TO-CARBON BONDS
    • C08G18/00—Polymeric products of isocyanates or isothiocyanates
    • C08G18/06—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen
    • C08G18/70—Polymeric products of isocyanates or isothiocyanates with compounds having active hydrogen characterised by the isocyanates or isothiocyanates used
    • C08G18/72—Polyisocyanates or polyisothiocyanates
    • C08G18/77—Polyisocyanates or polyisothiocyanates having heteroatoms in addition to the isocyanate or isothiocyanate nitrogen and oxygen or sulfur
    • C08G18/78—Nitrogen
    • C08G18/7806—Nitrogen containing -N-C=0 groups
    • C08G18/7818—Nitrogen containing -N-C=0 groups containing ureum or ureum derivative groups
    • C08G18/7837—Nitrogen containing -N-C=0 groups containing ureum or ureum derivative groups containing allophanate groups

Definitions

  • the present invention is directed to a process for the production of polyisocyanates which contain allophanate groups and isocyanurate groups and have a low viscosity and improved compatibility with polar and slightly polar solvents and isocyanate-reactive components.
  • Polyisocyanates containing isocyanurate groups are known and disclosed in U.S. Patents 3,487,080, 3,996,223, 4,324,879 and 4,412,073. While these polyisocyanates possess many outstanding properties, they do require improvement in two areas. First, the viscosity of commercially available polyisocyanates containing isocyanurate groups needs to be reduced in order to reduce the amount of solvent which is necessary to obtain a suitable processing viscosity. Presently, there are an increasing number of government regulations which limit the amount of volatile solvents which may be present in coating systems.
  • isocyanurate group-containing polyisocyanates may be precluded from certain applications because it is not possible to reduce the viscosity of these polyisocyanates to a suitable processing viscosity without using high amounts of solvent.
  • the isocyanurate group-containing polyisocyanates do not possess sufficient compatibility with highly branched polyester co-reactants as evidenced by the gloss and distinctness of image readings obtained from coatings prepared from these reactants.
  • polyisocyanates which have a reduced viscosity and improved compatibility with crosslinked polyester co-reactants, while possessing the desirable properties of known polyisocyanates containing isocyanurate groups. It is an additional object of the present invention to provide polyisocyanates which may be produced at reasonable production costs and which are obtained in high yields. Surprisingly, these objectives may be achieved in accordance with the present invention as described hereinafter by the incorporation of specific monoalcohols before or during the trimerization process in order to produce a polyisocyanate containing isocyanurate and allophanate groups.
  • U.S. Patents 4,582,888, 4,604,418, 4,647,623, 4,789,715 are directed the incorporation of various diols in order to improve the compatibility of the resulting polyisocyanates with certain solvents and co-reactants. While the use of diols may improve the compatibility of the polyisocyanates, the diols do not reduce the viscosity of the polyisocyanurates for a given yield.
  • polyisocyanates containing isocyanurate and allophanate groups in the presence of catalysts is known, e.g. from FR-A 1304301, EP-A 416338, FR-A 1215428, JP-A 61161179, EP-A 57653.
  • Japanese Publication 61-151179 discloses the use of monoalcohols containing 6 to 9 carbon atoms as co-catalysts for trimerization catalysts which do not trimerize HDI in the absence of a co-catalyst. This reference does not suggest the use of these monoalcohols in combination with trimerization catalysts which are effective for the trimerization reaction in the absence of co-catalysts.
  • the present invention is directed to a process for the production of a polyisocyanate composition having an NCO content of 10 to 47 % by weight and a viscosity of less than 1300 mPa.s (25° C), wherein the viscosity is determined from a mixture containing less than 1 % by weight of the starting organic diisocyanate, and containing isocyanurate and allophanate groups in a molar ratio of monoisocyanurates to monoallophanates of 10 : 1 to 1 : 5 which comprises
  • the term "monoisocyanurate” means a polyisocyanate containing one isocyanurate group and formed from three diisocyanate molecules
  • the term “polyisocyanurate” means a polyisocyanate containing more than one isocyanurate group.
  • the term “monoallophanate” means a polyisocyanate containing one allophanate group and formed from two diisocyanate molecules and 1 monoalcohol molecule
  • the term “polyallophattate” means a polyisocyanate containing more than one allophanate group.
  • (cyclo)aliphatically bound isocyanate groups” means aliphatically and/or cycloaliphatically bound isocyanate groups.
  • suitable diisocyanates to be used as starting materials for preparing the polyisocyanates according to the present invention are organic diisocyanates represented by the formula R(NCO) 2 wherein R represents an organic group obtained by removing the isocyanate groups from an organic diisocyanate having (cyclo)aliphatically bound isocyanate groups and a molecular weight of 112 to 1,000, preferably 140 to 400.
  • Preferred diisocyanates for the process according to the invention are those represented by the above formula wherein R represents a divalent aliphatic hydrocarbon group having from 4 to 18 carbon atoms, a divalent cycloaliphatic hydrocarbon group having from 5 to 15 carbon atoms or a divalent araliphatic hydrocarbon group having from 7 to 15 carbon atoms.
  • organic diisocyanates which are particularly suitable for the process include 1,4-tetramethylene diisocyanate, 1,6-hexamethylene diisocyanate, 2,2,4-trimethyl-1,6-hexamethylene diisocyanate, 1,12-dodecamethylenediisocyanate, cyclohexane-1,3- and -1,4-diisocyanate, 1-isocyanato-2-isocyanatomethyl cyclopentane, 1-isocyanato-3-isocyanatomethyl-3,5,5-trimethyl-cyclohexane (isophorone diisocyanate or IPDI), bis-(4-isocyanatocyclohexyl)-methane, 1,3- and 1,4-bis(isocyanatomethyl)-cyclohexane, bis-(4-isocyanato-3-methyl-cyclohexyl)-methane, ⁇ , ⁇ , ⁇ ', ⁇ '-tetramethyl-1
  • diisocyanates may also be used.
  • Preferred diisocyanates are 1,6-hexamethylene diisocyanate, isophorone diisocyanate and bis-(4-isocyanatocyclohexyl)-methane.
  • 1,6-hexamethylene diisocyanate (HDI) is especially preferred.
  • Trimerization catalysts which are suitable for the process according to the invention include compounds containing aminosilyl groups and those which are effective for the trimerization of polyisocyanates in the absence of a co-catalyst containing urethane groups, with the exception of phosphines, e.g., those described in DE-OS 1,935,763, and Mannich bases, for example, those based on nonylphenol, formaldehyde and dimethylamine of the type described in U.S. Patents 3,996,223 and 4,115,373.
  • the phosphines in addition to promoting the trimerization reaction, also promote the dimerization of diisocyanates.
  • the Mannich bases are generally used for the trimerization of aromatic polyisocyanates and are much less effective or not effective at all for the trimerization of (cyclo)aliphatic diisocyanates. Therefore, these catalysts are not suitable for preparing the products of the present invention.
  • the trimerization catalysts should also catalyze the formation of allophanate groups from urethane groups.
  • Catalysts which are effective for the trimerization of diisocyanates in the absence of a co-catalyst may be defined as those which are capable of reducing the isocyanate content of a mixture consisting of 1,6-hexamethylene diisocyanate containing less than 10 ppm of carbon dioxide and the trimerization catalyst from 50% to 45% by weight or less within a period of 4 hours at a catalyst concentration of 500 ppm, based on the weight of 1,6-hexamethylene diisocyanate, and a temperature of 80°C.
  • Particularly suitable catalysts which are effective for the trimerization of diisocyanates in the absence of a co-catalyst are quaternary ammonium hydroxides corresponding to the formula as described in U.S. Patent 4,324,879 and German Offenlegungsschriften 2,806,731 and 2,901,479.
  • Preferred quaternary ammonium hydroxides are those wherein the radicals R 1 to R 4 represent identical or different alkyl groups having from 1 to 20, preferably from 1 to 4 carbon atoms, which may optionally be substituted by hydroxyl groups.
  • Two of the radicals R 1 to R 4 may form a heterocyclic ring having from 3 to 5 carbon atoms together with the nitrogen atom and optionally with a further nitrogen or oxygen atom.
  • radicals R 1 to R 3 in each case may represent ethylene radicals which form a bicyclic triethylene diamine structure together with the quaternary nitrogen atom and a further tertiary nitrogen atom, provided that the radical R 4 then represents a hydroxyalkyl group having from 2 to 4 carbon atoms in which the hydroxyl group is preferably arranged in a 2-position to the quaternary nitrogen atom.
  • the hydroxyl-substituted radical or the hydroxyl-substituted radicals may also contain other substituents, particularly C 1 to C 4 -alkoxy substituents.
  • quaternary ammonium catalysts takes place in known manner by reacting a tertiary amine with an alkylene oxide in an aqueous-alcoholic medium (c.f. US-P 3,995,997, col. 2, lines 19-44).
  • suitable tertiary amines include trimethylamine, tributylamine, 2-dimethylaminoethanol, triethanolamine, dodecyldimethylamine, N,N-dimethylcyclohexylamine, N-methylpyrrolidine, N-methylmorpholine and 1,4-diazabicyclo-[2,2,2]-octane.
  • alkylene oxides examples include ethylene oxide, propylene oxide, 1,2-butylene oxide, styrene oxide and methoxy, ethoxy or phenoxy propylene oxide.
  • the most preferred catalysts from this group are N,N,N-trimethyl-N-(2-hydroxyethyl)-ammonium hydroxide and N,N,N-trimethyl-N-(2-hydroxypropyl)ammonium hydroxide.
  • Another most preferred catalyst is N,N,N-trimethyl-N-benzyl-ammonium hydroxide.
  • the trimerization of the starting diisocyanates may be carried out in the absence or in the presence of solvents which are inert to isocyanate groups.
  • solvents which are inert to isocyanate groups.
  • low to medium-boiling solvents or high-boiling solvents can be used.
  • Suitable solvents include esters such as ethyl acetate or butyl atetate; ketones such as atetone or butanone; aromatic compounds such as toluene or xylene; halogenated hydrocarbons such as methylene chloride and trithloroethylene; ethers such as diisopropylether; and alkanes such as cyclohexane, petroleum ether or ligroin.
  • the trimerization catalysts are generally used in quantities of about 0.0005 to 5% by weight, preferably about 0.002 to 2% by weight, based on the diisocyanate used. If, for example, a preferred catalyst such as N,N,N-trimethyl-N-(2-hydroxypropyl)-ammonium hydroxide is used, then quantities of about 0.0005 to 1% by weight, preferably about 0.001 to 0.02 by weight, based on starting diisotyanate, are generally sufficient.
  • the catalysts may be used in pure form or in solution.
  • the previously named solvents which are inert to isocyanate groups are suitable as solvents, depending on the type of catalysts. Dimethyl formamide or dimethyl sulphoxide may also be used as solvents for the catalysts.
  • co-catalysts are possible in the process according to the invention, but not necessary. All substances from which a polymerizing effect on isocyanates is known are suitable as co-catalysts such as those described in DE-OS 2,806,731.
  • the co-catalysts are optionally used in a lesser amount on a weight basis in relation to the amount of the trimerization catalyst.
  • urethane groups and subsequently allophanate groups are incorporated into the polyisocyanates by the use of monoalcohols.
  • the monoalcohols may be linear, branched or cyclic and contain 6 to 9, preferably 6 or 8 carbon atoms.
  • the monoalcohols may optionally contain ether groups. Examples of suitable monoalcohols include n-hexanol, n-heptanol, n-octanol, n-nonanol, 2-ethyl hexanol, trimethyl hexanol, cyclohexanol and benzyl alcohol.
  • the molar ratio of monoalcohol to diisocyanate is about 0.01 to 0.5, preferably about 0.04 to 0.2.
  • the reaction temperature for isocyanurate and allophanate formation in accordance with the present invention is about 10 to 160°C, preferably about 50 to 150°C and more preferably about 90 to 120°C.
  • the process according to the invention may take place either batchwise or continuously, for example, as described below.
  • the starting diisocyanate is introduced with the exclusion of moisture and optionally with an inert gas into a suitable stirred vessel or tube and optionally mixed with a solvent which is inert to isocyanate groups such as toluene, butyl acetate, diisopropylether or cyclohexane.
  • a solvent which is inert to isocyanate groups such as toluene, butyl acetate, diisopropylether or cyclohexane.
  • the previously described monoalcohol may be introduced into the reaction vessel in accordance with several embodiments.
  • the monoalcohol may be prereacted with the diisocyanate to form urethane groups prior to introducing the diisocyanate into the reaction vessel; the monoalcohol may be mixed with the diisocyanate and introduced into the reaction vessel; the monoalcohol may be separately added to the reaction vessel either before or after, preferably after, the diisocyanate is added; or the catalyst may be dissolved in the monoalcohol prior to introducing the solution into the reaction vessel.
  • the polyisocyanates according to the invention may also be prepared by blending polyisocyanates containing isocyanurate groups with monoallophonates.
  • the trimerization begins and is indicated by an exothermic reaction. As the reaction temperature increases the conversion rate of urethane groups to allophanate groups increases faster than the formation of isocyanurate groups. At temperatures above 85°C when the desired degree of trimerization is achieved, the urethane groups are generally completely converted to allophanate groups and the product, after removal of unreacted monomer and any solvent present has a low viscosity relative to the yield which is obtained. At temperatures below 85°C at the same degree of isocyanate group consumption, some urethane groups remain unconverted and the product has a slightly higher, but still low viscosity relative to the yield which is obtained.
  • the progress of the reaction is followed by determining the NCO content by a suitable method such as titration, refractive index or IR analysis.
  • the reaction may be terminated at the desired degree of trimerization.
  • the termination of the trimerization reaction can take place, for example, at an NCO content of about 15% to 47%, preferably about 20 to 40%.
  • the termination of the trimerization reaction can take place, for example, by the addition of a catalyst-poison of the type named by way of example in the above-mentioned literature references.
  • a catalyst-poison of the type named by way of example in the above-mentioned literature references.
  • the reaction is terminated by the addition of a quantity, which is at least equivalent to the catalyst quantity, of an acid chloride such as benzoyl chloride.
  • an acid chloride such as benzoyl chloride.
  • poisoning of the catalyst by the addition of a catalyst-poison may be dispensed with, since these catalysts decompose in the course of the reaction.
  • the catalyst quantity and the reaction temperature are preferably selected such that the catalyst which continuously decomposes is totally decomposed when the desired degree of trimerization is reached.
  • the quantity of catalyst or reaction temperature which is necessary to achieve this decomposition tan be determined by a preliminary experiment. It is also possible initially to use a lesser quantity of a heat sensitive catalyst than is necessary to achieve the desired degree of trimerization and to subsequently catalyze the reaction by a further incremental addition of catalyst, whereby the quantity of catalyst added later is calculated such that when the desired degree of trimerization is achieved, the total quantity of catalyst is spent.
  • the use of suspended catalysts is also possible. These catalysts are removed after achieving the desired degree of trimerization by filtering the reaction mixture.
  • the working-up of the reaction mixture may take place in various ways depending upon how the reaction was conducted and the area of application for the isocyanates. It is possible to use the polyisocyanates according to the invention which have been produced in solution directly as a lacquer raw material, without a purification stage, if it is not necessary to reduce the free monomer content. Any solvent used during trimerization reaction and any unreacted monomer present in the polyisocyanate product can also be removed by distillation in known manner.
  • the product generally contains a total of less than 2, preferably less than 1% of free (unreacted) monomeric diisocyanates.
  • the products according to the invention have a viscosity of less than 10,000 mPa.s, preferably less than 2000 mPa.s and more preferably less than 1300 mPa.s.
  • the products according to the present invention are polyisocyanates containing isocyanurate groups and allophanate groups.
  • the products may also contain residual urethane groups which have not been converted to allophanate groups depending upon the temperature maintained during the reaction and the degree of isocyanate group consumption.
  • the ratio of monoisocyanurate groups to monoallophanate groups present in the polyisocyanates according to the invention is about 10:1 to 1:5, preferably about 5:1 to 1:2.
  • the products according to the invention are valuable starting materials for the production of polyisocyanate polyaddition products by reaction with compounds containing at least two isocyanate reactive groups.
  • Preferred products are most preferably one or two-component polyurethane coatings.
  • Preferred reaction partners for the products according to the invention are the polyhydroxy polyesters, polyhydroxy polyethers, polyhydroxy polyacrylates and optionally low molecular weight, polyhydric alcohols known from polyurethane coatings technology.
  • Polyamines, particularly in blocked form, for example as polyketimines or oxazolidines are also suitable reaction partners for the products according to the invention.
  • the amounts of the polyisocyanates according to the invention and their reaction partners are selected to provide equivalent ratio of isocyanate groups (whether present in blocked or unblocked form) to isocyanate-reactive groups of about 0.8 to 3, preferably about 0.9 to 1.1.
  • the coating compositions may contain known polyurethane catalysts, e.g., tertiary amines such as triethylamine, pyridine, methyl pyridine, benzyl dimethylamine, N,N-dimethylamino cyclohexane, N-methylpiperidine, pentamethyl diethylene triamine, 1,4-diazabicyclo[2,2,2]-octane and N,N'-dimethyl piperazine; or metal salts such as iron(III)-chloride, zinc chloride, zinc-2-ethyl caproate, tin(II)-ethyl caproate, dibutyltin(IV)-dilaurate and molybdenum glycolate.
  • tertiary amines such as triethylamine, pyridine, methyl pyridine, benzyl dimethylamine, N,N-dimethylamino cyclohexane, N-methylpiperidine, pen
  • the products according to the invention are also valuable starting materials for two-component polyurethane stoving enamels in which the isocyanate groups are used in a form blocked by known blocking agents.
  • the blocking reaction is carried out in known manner by reacting the isocyanate groups with suitable blocking agents, preferably at an elevated temperature (e.g. about 40 to 160°C), and optionally in the presence of a suitable catalyst, for example, the previously described tertiary amines or metal salts.
  • Suitable blocking agents include monophenols such as phenol, the cresols, the trimethylphenols and the tert. butyl phenols; tertiary alcohols such as tert. butanol, tert. amyl alcohol and dimethylphenyl carbinol; compounds which easily form enols such as acetoacetic ester, acetyl acetone and malonic acid derivatives, e.g.
  • malonic acid diethylester secondary aromatic amines such as N-methyl aniline, the N-methyl toluidine, N-phenyl toluidine and N-phenyl xylidine; imides such as succinimide; lactams such as ⁇ -caprolactam and ⁇ -valerolactam; oximes such as butanone oxime and cyclohexanone oxime mercaptans such as methyl mercaptan, ethyl mercaptan, butyl mercaptan, 2-mercaptobenzthiazole, ⁇ -naphthyl mercaptan and dodecyl mercaptan; and triazoles such as 1H-1,2,4-triazole.
  • secondary aromatic amines such as N-methyl aniline, the N-methyl toluidine, N-phenyl toluidine and N-phenyl xylidine
  • imides such as succinimide
  • lactams such
  • the coating compositions may also contain other additives such as pigments, dyes, fillers, levelling agents and solvents.
  • the coating compositions may be applied to the substrate to be coated in solution or from the melt by conventional methods such as painting, rolling, pouring or spraying.
  • the coating compositions containing the polyisocyanates according to the invention provide coatings which adhere surprisingly well to a metallic base, and are particularly light-fast, color-stable in the presence of heat and very resistant to abrasion. Furthermore, they are characterized by high hardness, elasticity, very good resistance to chemicals, high gloss, excellent weather resistance and good pigmenting qualities.
  • the polyisocyanates according to the invention also possess good compatibility with highly branched polyester resins.

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  • Chemical & Material Sciences (AREA)
  • Organic Chemistry (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Polyurethanes Or Polyureas (AREA)
  • Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)

Claims (3)

  1. Verfahren zur Herstellung einer Polyisocyanatzusammensetzung mit einem NCO-Gehalt von 10 bis 47 Gew.-% und einer Viskosität von weniger als 1300 mPa·s (25°C), wobei die Viskosität an einem Gemisch bestimmt wird, das weniger als 1 Gew.-% des anfangs eingesetzten organischen Diisocyanats enthält, das Isocyanurat- und Allophanatgruppen in einem Stoffmengenverhältnis von Monoisocyanuraten zu Monoallophanaten von 10:1 bis 1:5 enthält, umfassend
    a) das katalytische Trimerisieren eines Teils der Isocyanatgruppen von Hexamethylendiisocyanat in Gegenwart von Trimethylbenzylammoniumhydroxid oder eines Trimerisierungskatalysators der Formel
    Figure imgb0005
     wobei R1 bis R4 gleiche oder verschiedene Alkylgruppen mit 1 bis 20 Kohlenstoffatomen darstellen, die mit Hydroxygruppen substituiert sein können, mit der Maßgabe, daß zwei der Reste R1 bis R4 zusammen mit dem Stickstoffatom und gegebenenfalls einem weiteren Stickstoffatom oder einem Sauerstoffatom einen heterocyclischen Ring mit 3 bis 4 Kohlenstoffatomen bilden können, oder wobei die Reste R1 bis R3 jeweils Ethylenreste darstellen können, die zusammen mit dem quartären Stickstoffatom und einem weiteren tertiären Stickstoffatom eine bicyclische Triethylendiaminstruktur bilden, mit der Maßgabe, daß der Rest R4 dann eine Hydroxyalkylgruppe mit 2 bis 4 Kohlenstoffatomen darstellt,
    b) das Hinzufügen von 0,01 bis 0,5 mol eines Monoalkohols, der 6 bis 9 Kohlenstoffatome enthält, pro Mol des organischen Diisocyanats zu dem organischen Diisocyanat vor oder während der Trimerisierungsreaktion von Schritt a),
    c) das Beenden der Trimerisierungsreaktion bei dem gewünschten Trimerisierungsgrad durch Hinzufügen eines Katalysatorgiftes und/oder durch thermisches Desaktivieren des Katalysators und
    d) Entfernen von nicht umgesetztem Hexamethylendiisocyanat durch Destillation bis zu einem Gehalt des Produkts an Hexamethylendiisocyanat von weniger als 1Gew.-%.
  2. Verfahren gemäß Anspruch 1, wobei der Monoalkohol 6 oder 8 Kohlenstoffatome enthält.
  3. Verfahren gemäß Anspruch 1 oder 2, wobei der Monoalkohol 2-Ethylhexanol umfaßt.
EP92111701A 1991-07-22 1992-07-09 Verfahren zur Herstellung von Allophanat- und Isocyanuratgruppen enthaltenden Polyisocyanaten Expired - Lifetime EP0524501B2 (de)

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US73354991A 1991-07-22 1991-07-22
US733549 1991-07-22

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EP0524501A1 EP0524501A1 (de) 1993-01-27
EP0524501B1 true EP0524501B1 (de) 1996-10-30
EP0524501B2 EP0524501B2 (de) 2005-08-31

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EP (1) EP0524501B2 (de)
JP (1) JPH05222007A (de)
CA (1) CA2072916C (de)
DE (1) DE69214890T3 (de)
ES (1) ES2093742T5 (de)

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CA2072916C (en) 2003-02-11
JPH05222007A (ja) 1993-08-31
EP0524501B2 (de) 2005-08-31
ES2093742T3 (es) 1997-01-01
EP0524501A1 (de) 1993-01-27
DE69214890D1 (de) 1996-12-05
DE69214890T3 (de) 2006-03-23
DE69214890T2 (de) 1997-02-27
CA2072916A1 (en) 1993-01-23
ES2093742T5 (es) 2006-02-16

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